Method for producing fiber reinforced cementitious slurry using a multi-stage continuous mixer

ABSTRACT

A method in which a stream of dry cementitious powder from a dry powder feeder passes through a dry cementitious powder inlet conduit to feed a first feed section of a fiber-slurry mixer. An aqueous medium stream passes through at least one aqueous medium stream conduit to feed a first mixing section the fiber-slurry mixer. A stream of reinforcing fibers passes from a fiber feeder through a reinforcing fibers stream conduit to feed a second mixing section of the fiber-slurry mixer. The stream of dry cementitious powder, aqueous medium stream, and stream of reinforcing fibers combine in the fiber-slurry mixer to make a stream of fiber-cement mixture which discharges through a discharge conduit at a downstream end of the mixer.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is related to:

-   U.S. Provisional Patent Application No. 62/371,554 filed Aug. 5,    2016, entitled CONTINUOUS METHODS OF MAKING FIBER REINFORCED    CONCRETE PANELS, filed Aug. 5, 2016;-   U.S. Provisional Patent Application No. 62/371,569 filed Aug. 5,    2016, entitled HEADBOX AND FORMING STATION FOR FIBER REINFORCED    CEMENTITIOUS PANEL PRODUCTION, filed Aug. 5, 2016;-   U.S. Provisional Patent Application No. 62/371,578 filed Aug. 5,    2016, entitled CONTINUOUS MIXER AND METHOD OF MIXING REINFORCING    FIBERS WITH CEMENTITIOUS MATERIALS, filed Aug. 5, 2016;

all herein incorporated by reference in their entirety.

This application claims the benefit of U.S. Provisional PatentApplication No. 62/371,590 entitled A METHOD FOR PRODUCING FIBERREINFORCED CEMENTITIOUS SLURRY USING A MULTI-STAGE CONTINUOUS MIXER,filed Aug. 5, 2016 incorporated by reference in its entirety.

FIELD OF THE INVENTION

This invention discloses a continuous mixer and a method of mixingreinforcing fibers with cementitious materials for producing fiberreinforced cementitious materials, namely (fiber reinforced concrete(FRC) panel), in a continuous process.

BACKGROUND OF THE INVENTION

U.S. Pat. No. 6,986,812 of Dubey et al., incorporated herein byreference in its entirety, features a slurry feed apparatus for use in aSCP panel production line or the like application where settableslurries are used in the production of building panels or board. Theapparatus includes a main metering roll and a companion roll placed inclose, generally parallel relationship to each other to form a nip inwhich a supply of slurry is retained. Both rolls preferably rotate inthe same direction so that slurry is drawn from the nip over themetering roll to be deposited upon a moving web of the SCP panelproduction line. A thickness control roll is provided in closeoperational proximity to the main metering roll for maintaining adesired thickness of the slurry.

U.S. Pat. No. 7,524,386 B2 to George et al, incorporated herein byreference in its entirety, discloses a process employing a wet mixerhaving a vertical mixing chamber for forming a wet slurry of acementitious powder and liquid. The vertical mixing chamber is designedto provide the required amount of mixing to provide thoroughly mixed,uniformly thin slurry within a mixing residence time that allows foradequate supply of slurry to ensure continuous operation of anassociated cement panel production line. Gravity feed means for supplyof cementitious powder and water to the slurry mixing area of thechamber is also disclosed. In preparing the SCP panels, an importantstep is mixing cementitious powder to form slurry. The slurry is thenwithdrawn from the bottom of the chamber and pumped through a cavitypump to the slurry feeding apparatus. A typical conventional continuouscement mixer is the DUO MIX2000 continuous cement mixer from M-TEC GmbH,Neuenburg, Germany which is used in the construction industry to mix andpump concrete slurry.

U.S. Pat. No. 7,513,963 B2 to George et al, incorporated herein byreference in its entirety, discloses a wet mixer apparatus and methodfor its use, the mixer having a vertical mixing chamber for forming awet slurry of a cementitious slurry and water. The vertical mixingchamber is designed to provide the required amount of mixing to providethoroughly mixed, uniformly thin slurry within a mixing residence timethat allows for adequate supply of slurry to ensure continuous operationof an associated cement panel production line. Gravity feeding forseparate supply of cementitious powder and water to the slurry mixingarea of the chamber without pre-mixing of the powder and water is alsodisclosed.

U.S. Pat. No. 8,038,790 to Dubey et al., incorporated herein byreference in its entirety, discloses structural cement panel forresisting transverse and shear loads equal to transverse and shear loadsprovided by plywood and oriented strain board, when fastened to framingfor use in shear walls, flooring and roofing systems. The panels providereduced thermal transmission compared to other structural cement panels.The panels employ one or more layers of a continuous phase resultingfrom curing an aqueous mixture of calcium sulfate alpha hemihydrate,hydraulic cement, coated expanded perlite particles filler, optionaladditional fillers, active pozzolan and lime. The coated perlite has aparticle size of 1-500 microns, a median diameter of 20-150 microns, andan effective particle density (specific gravity) of less than 0.50 g/cc.The panels are reinforced with fibers, for example alkali-resistantglass fibers.

US Patent Application Publication No. 2005/0064164 to Dubey et al.,incorporated herein by reference in its entirety, discloses amulti-layer process for producing structural cementitious panel whichincludes: (a.) providing a moving web; (b.) one of (i) depositing afirst layer of individual, loose fibers upon the web, followed bydepositing a layer of settable slurry upon the web and (ii) depositing alayer of settable slurry upon the web; (c.) depositing a second layer ofindividual, loose fibers upon the slurry; (d.) actively embedding saidsecond layer of individual, loose fibers into the slurry to distributesaid fibers throughout the slurry; and (e.) repeating steps (ii) through(d.) until the desired number of layers of settable fiber-enhancedslurry is obtained and so that the fibers are distributed throughout thepanel. Also provided are a structural panel produced by the process, anapparatus suitable for producing structural cementitious panelsaccording to the process, and a structural cementitious panel havingmultiple layers, each layer created by depositing a layer of settableslurry upon a moving web, depositing fibers upon the slurry andembedding the fibers into the slurry such that each layer is integrallyformed with the adjacent layers.

US Patent Application Publication No. 2006/0061007 to Chen discloses amethod and apparatus for extruding cementitious articles. The extruderincludes a casing with a pair of inter-meshing self-wiping screwsrotatably mounted therein. The screws continuously mix and knead thecomponents of the fiber cement provided through various feed means toform a substantially homogeneous paste and force the paste through a dieto form a green cementitious extrudate suitable for casting.Cementitious mixtures for extruding are very viscous and not suitablefor uses such as shotcrete or deposition through a headbox on acementitious panel production line.

The current state-of-the-art mixing technology for producing fiberreinforced cementitious slurry typically involves use of industrystandard batch mixers into which all raw materials including reinforcingfibers are first added and then mixed for several minutes to yield aslurry mixture with randomly dispersed fibers. Rotating drum androtating pan mixers are examples of concrete mixers that are commonlyused for preparing fiber reinforced cementitious slurry mixtures. Somemajor limitations and drawbacks of the current state-of-the art concretemixers and mixing technologies for producing fiber reinforcedcementitious slurry mixtures include:

The mixing operation in a batch mixer is not continuous thus makingtheir use more difficult in applications where a continuous supply ofslurry is needed such as in the case of a continuous panel productionline.

The mixing time in a batch mixer is typically very long, in the order ofseveral minutes, to obtain a well-blended, homogeneous slurry mixture.

Since a large amount of fibers are added at a time in a batch mixer,that leads to fiber lumping and balling during the mixing operation.

Longer mixing times involved with the batch mixing process tend todamage and break the reinforcing fibers.

Batch mixers are not very useful and practical with respect to handlingrapid setting cementitious materials.

There is a need for a single-layer process for producing slurry forcementitious panels having high reinforcing fiber concentrations. Thus,there is a need for an improved wet mixing apparatus that ensures supplyof sufficient mixed fluid cementitious slurry which contains glassfibers to supply a continuous panel production line. It is desired toprovide a degree of mixing of the cementitious reactive powder, glassfibers, and water in the mixer to result in a slurry of proper rheologyand sufficient fluidity to provide a slurry for use in the continuouscementitious panel manufacturing line.

SUMMARY OF THE INVENTION

The present invention uses a wet mixer apparatus for preparing slurry tobe fed to a slurry feed apparatus (typically known as a “headbox”) foruse in depositing slurry on a moving web of a cementitious panelproduction line or the like where settable slurries are used forproducing fiber reinforced building panels or boards.

Considering the limitations and drawbacks of the currentstate-of-the-art concrete mixers, some objectives of the presentinvention are as follows:

Provide a mixer that allows continuous blending of fibers with the restof the cementitious components to produce a uniformly mixed fiberreinforced cementitious slurry mixture.

Provide a mixer that reduces the required mixing time from severalminutes to less than 60 seconds, preferably less than 30 seconds, toproduce a uniformly blended fiber reinforced cementitious slurrymixture.

Provide a mixer that does not cause fiber balling and lumping during themixing operation.

Provide a mixer that does not cause damage to the reinforcing fibers asa result of the mixing action.

The invention provides a method for preparing cement composite slurrywhich can be supplied in a continuous manner comprising the steps of:

feeding a dry cementitious powder into a horizontal continuous mixerthrough at least one dry cementitious powder inlet port;

the horizontal continuous mixer comprising

-   -   an elongated mixing chamber, the elongated mixing chamber        defined by a horizontal (typically cylindrical) housing having        an interior side wall, the elongated mixing chamber having an        upstream end feed section, a first mixing section, and a second        downstream end mixing section, wherein the first mixing section        is between the upstream end feed section and the second        downstream end mixing section,    -   at least a pair of horizontally oriented intermeshing        self-wiping impellers traversing from an upstream end of the        elongated mixing chamber to a downstream end of the elongated        mixing chamber and rotating within the elongated mixing chamber,

wherein each horizontally mounted impeller within the upstream end feedsection of the elongated mixing chamber comprises an auger, wherein thedry cementitious powder is fed into the upstream end feed section of theelongated mixing chamber and conveyed by the auger to the first mixingsection,

feeding a liquid stream comprising water into the elongated mixingchamber of the continuous slurry mixer through at least one liquidstream inlet port downstream of the at least one dry cementitious powderinlet port and mixing the dry cementitious powder and the liquid streamin the first mixing section to form a cementitious slurry;

wherein each horizontally mounted impeller within the first mixingsection comprises a first plurality of mixing paddles mounted on ahorizontally oriented shaft of the impeller at regular intervals anddifferent circumferential locations, the paddles rotated about thehorizontally oriented shaft within the horizontal, preferablycylindrical housing, the paddles extending radially from the shaft,

feeding a stream of reinforcement fibers through at least onereinforcement fiber inlet port into the second mixing section, andmixing the cementitious slurry and the reinforcement fibers in thesecond mixing section to form a fiber-slurry mixture,

wherein at least a portion of each horizontally mounted impeller withinthe second mixing section of the elongated mixing chamber comprises atleast one member selected from the group consisting of:

-   -   an auger, and    -   a second plurality of mixing paddles mounted on the horizontally        oriented shaft of the mixer at regular intervals and different        circumferential locations, the paddles rotated about each        respective horizontally oriented shaft within the horizontal        (preferably cylindrical) housing, the paddles extending radially        from the respective shaft,

discharging the fiber-slurry mixture from the mixer through afiber-slurry mixture outlet port at a downstream end portion of thesecond mixing section,

wherein the cementitious slurry and fibers are mixed in the mixingchamber of the horizontal continuous mixer for an average mixingresidence time of about 5 to about 240 seconds, preferably 10 to 180seconds, more preferably 10 to 120 seconds, most preferably 10 to 60seconds, while the rotating paddles apply shear force, wherein thecentral rotating shaft rotates at 30 to 450 RPM, more preferably 40 to300 RPM, and most preferably 50 to 250 RPM during mixing, to thefiber-slurry mixture to produce a uniform fiber-slurry mixture, whereinthe fiber-slurry mixtures discharged from the horizontal continuousmixer have a slump of 4 to 11 inches as measured according to a slumptest using a 4 inch tall and 2 inch diameter pipe.

The resulting fiber-slurry mixtures also have a viscosity less than45000 centipoise, preferably less than 30000 centipoise, more preferablyless than 15000 centipoise, and most preferably less than 10000centipoise when measured using a Brookfield Viscometer, Model DV-II+ Prowith Spindle HA4 attachment running at 20 RPM speed. Typically theresulting fiber-slurry mixtures have a viscosity of at least 1500centipoise. The fiber-slurry mixtures typically also includeplasticizers and superplasticizers. Plasticizers are commonlymanufactured from lignosulfonates, a by-product from the paper industry.Superplasticizers have generally been manufactured from sulfonatednaphthalene condensate or sulfonated melamine formaldehyde, or based onpolycarboxylic ethers.

The term paddles means any structure extending radially from the shaftfor rotating about the shaft. Paddles may have any of a variety ofshapes. For example, preferred paddles are flat paddles, helicalpaddles, or paddles made of a pin having opposed ends, one end forattaching to the shaft and the other end for attachment to a broadpaddle head. The pins used without the paddle head are also consideredpaddles within the scope of the invention.

The present fiber-slurry mixtures preferably lack thickeners or otheradditives that substantially increase material viscosity.

Each horizontally oriented shaft is externally connected to a drivemechanism and a drive motor, for example, powered by electricity, fuelgas, gasoline, or other hydrocarbon, to accomplish shaft rotation whenthe mixer is in operation.

The fiber-slurry mixtures discharged from the fiber-slurry mixer aresuitable for a variety of uses, for example statuary, shotcrete,consolidation of loose rock on slopes, soil stabilization, tunnel andmine linings, pre-cast concrete products, pavements and bridge decks,concrete slab-on-grade, repair applications, or to make a fiberreinforced cement building panel or board.

When using the settable fiber-slurry mixture for producing fiberreinforced cement panel (also known as a fiber reinforced concretepanel, abbreviated FRC panel) the fiber-slurry mixture is fed to aslurry feed apparatus (known as a “headbox”) which deposits thefiber-slurry mixture on a moving surface of a panel production lineuniformly as a layer 0.125 to 2 inches thick, preferably 0.25 to 1inches thick, typically 0.40 to 0.75 inches thick to produce the fiberreinforced concrete panel. The process for producing cementitious panelsfrom fiber-slurry mixtures of the present invention produces panelshaving at most a single layer of fiber reinforced cementitious slurry.Preferably the moving surface moves at a speed of 1 to 100 feet perminute, more preferably 5 to 50 feet per minute. This is substantiallyfaster than conventional extrusion processes well known in the art.Preferably the slurry is deposited on the moving surface at a rate of0.10 to 25 cubic feet per minute for a board ranging from 4 to 8 feetwide. The manufacturing process of this invention is also substantiallyfaster than conventional extrusion processes that utilize cementitiousmixtures having extremely high viscosities.

The resulting fiber-slurry mixtures of the present invention distinguishover cementitious mixtures used in extrusion processes. Such extrusionmixtures have a slump of 0 to 2 inches as measured according to theslump test using a 4 inch tall and 2 inch diameter pipe and have aviscosity greater than 50000 centipoise. The extrusion mixtures also donot include plasticizers and superplasticizers which are present infiber-slurry mixtures of the present invention. As mentioned aboveplasticizers are commonly manufactured from lignosulfonates, aby-product from the paper industry. Superplasticizers have generallybeen manufactured from sulfonated naphthalene condensate or sulfonatedmelamine formaldehyde, or based on polycarboxylic ethers.

A distinctive feature of the mixer and mixing method of the presentinvention disclosed herein is the ability of this mixer to blendreinforcing fibers with the rest of the cementitious components in acontinuous operation without unduly damaging the added fibers.Furthermore, the mixer and mixing method of this invention allowproduction of a fiber reinforced cementitious slurry mixture having adesirable working consistency. The slurries with favorable rheologicalproperties produced by this mixer can beneficially be utilized forproducing products using a variety of manufacturing processes. Forinstance, a workable slurry consistency facilitates further processingand formation of panel products on a continuous forming line running athigh line speeds.

Preferably, the paddles of the mixer comprise both members of the groupconsisting of:

-   -   the paddles of the first plurality of mixing and conveying        paddles which each comprise a pin engaged to a paddle head, the        pin pivotally engaged to the horizontally oriented shaft and/or        the paddle head to permit pivotal rotation of the paddle head        relative to the respective location on the horizontally oriented        shaft, wherein the plurality of paddles are arranged for mixing        the dry cementitious powder and the liquid stream to form a        cementitious slurry and move the cementitious slurry to the        second mixing section, and    -   the paddles of the second plurality of mixing and conveying        paddles which each comprise a pin engaged to a paddle head, the        pin pivotally engaged to the horizontally oriented shaft and/or        the paddle head to permit pivotal rotation of the paddle head        relative to the respective location on the horizontally oriented        shaft, wherein the plurality of paddles are arranged to mix the        reinforcement fibers and cementitious slurry and move the        cementitious slurry and reinforcement fibers being mixed to the        fiber-slurry mixer outlet.

Preferably the mixing chamber of the horizontal mixer is adapted andconfigured to mix the cementitious slurry and fibers in the mixingchamber of the horizontal mixer for an average mixing residence time ofabout 5 to about 240 seconds, preferably 10 to 180 seconds, morepreferably 10 to 120 seconds, most preferably 10 to 60 seconds while therotating paddles apply shear force, wherein the central rotating shaftrotates at 30 to 450 RPM, more preferably 40 to 300 RPM, and mostpreferably 50 to 250 RPM during mixing, to the fiber-slurry mixture toproduce a uniform fiber-slurry mixture as described above that has aconsistency to allow the fiber-slurry mixture to be discharged from thefiber-slurry mixer.

The mixer of the present invention may be employed as part of anapparatus for producing a cementitious panel having at most a singlelayer of fiber reinforced cementitious composition which includes aconveyor-type frame supporting a moving web; a first water andcementitious material mixer in operational relationship to the frame andconfigured for feeding the cementitious slurry into the fiber-slurrymixer; a first slurry feed station (headbox) in operational relationshipto the frame and configured for depositing a layer of settablefiber-containing cementitious slurry upon the moving web. Downstream isan apparatus for cutting the set slurry into cement boards.

The method disclosed herein is a continuous method as opposed to a batchmethod. In a continuous method the raw materials required to make theend product are metered and fed continuously at a rate that equals therate (mass balance) at which the end product is being produced, that is,the raw material feed flows in the process and the end product flows outof the process simultaneously. In a batch method, the raw materialsrequired to make the end product are first combined in large amounts toprepare a large batch of mixture for storage in appropriate vessel/s;this batch of mixture is then subsequently drawn from the storagevessel/s to produce multiple pieces of the end product.

In this specification all composition percentages are in weight percentunless otherwise indicated.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 shows a block flow diagram of the method of the presentinvention.

FIG. 2A shows an auger section at the mixer inlet and flat paddlesmounted on the two shafts in the first mixing section of the horizontaldual shaft multi-stage continuous fiber-slurry mixer embodiment of thepresent fiber-slurry mixing device.

FIG. 2B shows a portion of the auger section at the mixer dry powderinlet in a horizontal dual shaft multi-stage continuous fiber-slurrymixer embodiment of the present fiber-slurry mixing device.

FIG. 2C shows a flat mixing paddle of the horizontal dual shaftmulti-stage continuous fiber-slurry mixer embodiment of the presentfiber-slurry mixing device.

FIG. 2D shows a helical mixing paddle suitable for use in the horizontaldual shaft multi-stage continuous fiber-slurry mixer embodiment of thepresent fiber-slurry mixing device.

FIG. 2E shows flat paddles mounted on the two shafts in the first mixingsection of the horizontal dual shaft multi-stage continuous fiber-slurrymixer embodiment of the present fiber-slurry mixing device.

FIG. 2F shows flat paddles and a helical paddle on a shaft.

FIG. 3A shows a first configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer of the present invention in which thefirst section has mixing paddles and the second mixing section has onlyaugers on both shafts.

FIG. 3B shows a second configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer of the present invention in which thefirst mixing section has paddles and the second mixing section hasaugers followed by paddles on both shafts.

FIG. 3C shows a third configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer of the present invention in which thefirst mixing section has paddles and the second mixing section has anauger followed by paddle/s followed by an auger on both shafts.

FIG. 3D shows a fourth configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer of the present invention in which thefirst mixing section has paddles and the second mixing section has onlypaddles or pins on both shafts.

FIG. 4A shows a diagrammatic elevational side view of the configuration(schematically shown in FIG. 3D) of the horizontal dual-shaft (one shaftshown) multi-stage continuous fiber-slurry mixer of the presentinvention in which the first mixing section has paddles and the secondmixing section has only paddles.

FIG. 4B shows a perspective view of a paddle (with a pin and a head) ofthe horizontal fiber-slurry mixer embodiment of the present fiber-slurrymixing device of FIG. 4A.

FIG. 4C shows a top view of a paddle (with a pin and a head) and aportion of the shaft of the horizontal continuous fiber-slurry mixerembodiment of the present fiber-slurry mixing device of FIG. 4A.

FIG. 4D provides a close-up view of the mixer with a door to the mixingchamber of the present fiber-slurry mixing device of FIG. 4A openshowing the orientation of the paddles (with a pin and a head) withrespect to the central shaft (one shaft shown for clarity).

FIG. 4E shows a configuration (schematically shown in FIG. 3B) of adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixerin which the first mixing section has paddles and the second mixingsection has augers followed by paddles on both shafts.

FIG. 4F shows a configuration of a dual-shaft (one shaft shown)multi-stage continuous fiber-slurry mixer (schematically shown in FIG.3C) in which the first mixing section has paddles and the second mixingsection has an auger followed by paddle/s followed by an auger on bothshafts (one shaft shown for clarity).

FIG. 4G shows a configuration (schematically shown in FIG. 3B) of adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixerin which the first mixing section has paddles and the second mixingsection has an auger followed by pin/s followed by an auger on bothshafts.

FIG. 4H shows a configuration (schematically shown in FIG. 3D) of ahorizontal dual-shaft (one shaft shown) multi-stage continuousfiber-slurry mixer of the present invention in which the first mixingsection has paddles and the second mixing section has only pins on bothshafts.

FIG. 4I shows a configuration (schematically shown in FIG. 3A) having adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixerof the present invention in which the first mixing section has paddlesand the second mixing section has augers on both shafts), wherein thepaddles are flat paddles or helical paddles.

FIG. 4J shows a configuration (schematically shown in FIG. 3B) having adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixerof the present invention in which the first mixing section has paddlesand the second mixing section has augers followed by paddles on bothshafts (one shaft shown for clarity), wherein the paddles are flatpaddles or helical paddles, the empty space between paddles where theshaft is visible is intended to convey presence of paddles.

FIG. 4K shows a configuration (schematically shown in FIG. 3C) in whichthe first mixing section has flat paddle's and/or helical paddle/s andthe second mixing section has an auger followed by flat paddle's and/orhelical paddle/s followed by an auger on both shafts (one shaft shownfor clarity), wherein the paddles are flat paddles or helical paddles;the empty space between paddles where the shaft is visible is intendedto convey presence of paddles.

FIG. 4L shows a configuration (schematically shown in FIG. 3D) having adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixerof the present invention in which the first mixing section has paddlesand the second mixing section has paddles on both shafts, wherein thepaddles are flat paddles or helical paddles; the empty space where theshaft is visible is intended to convey presence of paddles.

FIG. 4M shows a variation of the configuration (schematically shown inFIG. 3D) having a dual-shaft (one shaft shown) multi-stage continuousfiber-slurry mixer of the present invention in which first mixingsection can have one type of paddles and the second mixing section canhave a different type of paddles; the preferred arrangement in thisconfiguration is to have flat paddles and/or helical paddles in thefirst mixing section and paddles with a pin and a head and/or only pins,in the second mixing section 24.

FIG. 5 shows a diagrammatic elevational view of a cementitious panelproduction line suitable for use with the present fiber-slurry mixingdevice.

FIG. 6 shows the cementitious panel production line of FIG. 5 as acomposite view of a process flow chart for the portion of thecementitious panel production line upstream of the headbox and a topview of the cementitious panel production line downstream of theheadbox.

FIG. 7 shows a first variation of the cementitious panel production lineof FIG. 5 as a composite view of a process flow chart for the portion ofthe cementitious panel production line suitable for use with the presentfiber-slurry mixing device upstream of the headbox and a top view of theproduction line downstream of the headbox.

FIG. 8 shows a second variation of the cementitious panel productionline of FIG. 5 as a composite view of a process flow chart for theportion of the cementitious panel production line suitable for use withthe present fiber-slurry mixing device upstream of the headbox and a topview of the production line downstream of the headbox.

DETAILED DESCRIPTION OF THE INVENTION

FIG. 1 shows a block flow diagram of the method of the presentinvention. In the method stream 5 of dry cementitious powder from a drypowder feeder 2 passes through a dry cementitious powder inlet conduit5A to feed a first feed section 20 of a fiber-slurry mixer 32. Anaqueous medium stream 7 from one or more pumps 3 passes through at leastone aqueous medium stream conduit 7A (two shown) to feed a first mixingsection 22 and optionally also the first feed section 20 of thefiber-slurry mixer 32. A stream 34 of reinforcing fibers passes from afiber feeder 33 through a reinforcing fibers stream conduit 34A to feeda second mixing section 24 of the fiber-slurry mixer 32. The stream 5 ofdry cementitious powder, aqueous medium stream 7, and stream 34 ofreinforcing fibers combine in the fiber-slurry mixer 32 to make a streamof fiber-cement mixture 36 which discharges through a discharge conduit36A at a downstream end of the mixer 32.

The resulting fiber-slurry mixture is suitable for a variety of uses.For example, the resulting slurry is suitable for being deposited andused as statuary, shotcrete, consolidation of loose rock, soilstabilization, pre-cast concrete products, pavement, repair application,or as a layer on a moving surface of a panel production line uniformlyas a layer 0.125 to 2.00 inches thick, preferably 0.25 to 1 inchesthick, more preferably 0.4 to 0.8 inches thick, typically 0.5 to 0.75inches thick on the moving surface of the panel production line toproduce a fiber reinforced concrete panel. The resulting fiber-slurrymixture has a viscosity less than 45000 centipoise, preferably less than30000 centipoise, and more preferably less than 15000 centipoise.Typically the resulting fiber-slurry mixtures have a viscosity of atleast 1500 centipoise. The resulting fiber-slurry mixture also has aslump according to the slump test using a 4 inch tall 2 inch diameterpipe is from 4 to 11 inches. The resulting fiber-slurry mixture is notsuitable for extrusion manufacturing processes that typically rely onslurry mixture compositions having extremely high viscosity.

The slump test characterizes the slump and flow behavior of thecementitious compositions produced by this invention. The slump testused herein utilizes a hollow cylinder about 5.08 cm. (2 in.) diameterand about 10.16 cm. (4 in.) length held vertically with one open endresting on a smooth plastic surface. The cylinder is filled up to thetop with the cementitious mixture followed by striking off the topsurface to remove the excess slurry mixture. The cylinder is then gentlylifted up vertically to allow the slurry to come out from the bottom andspread on the plastic surface to form a circular patty. The diameter ofthe patty is then measured and recorded as the slump of the material. Asused herein, compositions with good flow behavior yield a larger slumpvalue.

As seen in FIGS. 3A-3D and 4A-4M the invention employs the followingprimary mixer variations:

-   -   Mixer Dry Powder Inlet    -   Auger (to move the dry powder to the first mixing section with        paddles)    -   First Mixing Section—Paddles (one type or another)    -   Second Mixing Section—Various scenarios possible—Only Auger,        Only Paddles, or a combination of augers and paddles.        Horizontal Fiber-Slurry Continuous Mixer

The fiber-slurry continuous mixer of the present invention preferablyachieves the following results:

Allows continuous blending of fibers with the rest of the cementitiouscomponents to produce a uniformly mixed fiber reinforced cementitiousslurry mixture.

Reduces the required mixing time from several minutes to less than 60seconds, preferably less than 30 seconds, to produce a uniformly blendedfiber reinforced cementitious slurry mixture. Generally the chamberprovides an average slurry residence time of about 5 to about 240seconds, preferably 10 to 180 seconds, more preferably 10 to 120seconds, most preferably 10 to 60 seconds.

Does not cause fiber balling and lumping during the mixing operation.

Does not cause damage to the reinforcing fibers as a result of themixing action.

Allows use of rapid setting cementitious materials useful inmanufacturing and construction applications.

The method of using the horizontal fiber-slurry continuous mixerdisclosed as part of this invention comprising the steps of:

feeding a dry cementitious powder into a horizontal continuous slurrymixer through at least one dry cementitious powder inlet port;

the horizontal continuous mixer comprising

-   -   an elongated mixing chamber, the elongated mixing chamber        defined by a horizontal (typically cylindrical) housing having        an interior side wall, the elongated mixing chamber having an        upstream end feed section, a first mixing section, and a second        downstream end mixing section, wherein the first mixing section        is between the upstream end feed section and the second        downstream end mixing section,    -   at least a pair of horizontally oriented intermeshing        self-wiping impellers traversing from an upstream end of the        elongated mixing chamber to a downstream end of the elongated        mixing chamber and rotating within the elongated mixing chamber,

wherein each horizontally mounted impeller within the upstream end feedsection of the elongated mixing chamber comprises an auger, wherein thedry cementitious powder is fed into the upstream end feed section of theelongated mixing chamber and conveyed by the auger to the first mixingsection,

feeding a liquid stream comprising water into the elongated mixingchamber of the continuous slurry mixer through at least one liquidstream inlet port downstream of the at least one dry cementitious powderinlet port and mixing the dry cementitious powder and the liquid streamin the first mixing section to form a cementitious slurry;

wherein each horizontally mounted impeller within the first mixingsection comprises a first plurality of mixing and conveying paddlesmounted on a horizontally oriented shaft of the impeller at regularintervals and different circumferential locations, the paddles rotatedabout the horizontally oriented shaft within the horizontal, preferablycylindrical, housing, the paddles extending radially from the shaft,

feeding a stream of reinforcement fibers through at least onereinforcement fiber inlet port into the second mixing section, andmixing the cementitious slurry and the reinforcement fibers in thesecond mixing section to form a fiber-slurry mixture,

wherein at least a portion of each horizontally mounted impeller withinthe second mixing section of the elongated mixing chamber comprises atleast one member selected from the group consisting of:

-   -   an auger, and    -   a second plurality of mixing and conveying paddles mounted on        the horizontally oriented shaft of the mixer at regular        intervals and different circumferential locations, the paddles        rotated about each respective horizontally oriented shaft within        the horizontal (preferably cylindrical) housing, the paddles        extending radially from the respective shaft,

discharging the fiber-slurry mixture from the mixer through afiber-slurry mixture outlet port at a downstream end portion of thesecond mixing section,

wherein the cementitious slurry and fibers are mixed in the mixingchamber of the horizontal continuous mixer for an average mixingresidence time of about 5 to about 240 seconds, preferably 10 to 180seconds, more preferably 10 to 120 seconds, most preferably 10 to 60seconds while the rotating paddles apply shear force, wherein thecentral rotating shaft rotates at 30 to 450 RPM, more preferably 40 to300 RPM, and most preferably 50 to 250 RPM during mixing, to thefiber-slurry mixture to produce a uniform fiber-slurry mixture, whereinthe fiber-slurry mixture discharged from the mixer has a slump of 4 to11 inches, preferably 6 to 10 inches, as measured according to a slumptest using a 4 inch tall and 2 inch diameter pipe and a viscosity lessthan 45000 centipoise, preferably less than 30000 centipoise, and morepreferably less than 15000 centipoise.

The resulting fiber-slurry mixture also has a slump according to theslump test using a 4 inch tall 2 inch diameter pipe is from 4 to 11inches. The resulting fiber-slurry mixture is not suitable for extrusionmanufacturing processes that typically rely on slurry mixturecompositions having extremely high viscosity.

Each horizontally oriented shaft is externally connected to a drivemechanism and a drive motor, for example, powered by electricity, fuelgas, gasoline, or other hydrocarbon, to accomplish shaft rotation whenthe mixer is in operation.

The paddles of the first and/or second mixing sections may be flatpaddles or helical paddles. Flat paddles and helical paddles are unitarypaddles having a central opening fitted to the shaft such that thepaddle encircles a portion of the shaft. Also, the flat paddles andhelical paddles have opposed ends extending in opposite directions fromthe shaft. Preferably if the flat paddles or helical paddles areemployed in the second mixing section they are employed in a paddleportion of the second mixing section and an auger is also employed inthe second mixing section before and/or after the paddle section.

However, in the alternative the paddle of the first and/or second mixingsections comprises a pin engaged to a broad paddle head, the pinpivotally engaged to the horizontally oriented shaft and/or the paddlehead to permit pivotal rotation of the paddle head relative to therespective location on the horizontally oriented shaft, wherein thepaddles are arranged to mix the reinforcement fibers and cementitiousslurry and move the cementitious slurry and reinforcement fibers beingmixed to the fiber-slurry mixture outlet. Preferably if the paddles ofthe first and second mixing section each comprise the pin engaged to thepaddle head then the second mixing section has an absence of an auger.The second mixing section can optionally have only pins (without paddlehead) to mix fibers with the slurry. The cross-sectional shape of thepin can either be round, flat (i.e., square or rectangular), triangular,oval or any other shape. When pins with elongated cross-section areemployed (example, rectangular or oval cross-section), the pins arepreferably oriented such that they not only help to mix the material butalso provide the function of moving the material forward toward themixer outlet.

The central shaft is externally connected to a drive mechanism and adrive motor, for example, powered by electricity, fuel gas, gasoline, orother hydrocarbon, to accomplish shaft rotation when the mixer is inoperation. Typically an electrical motor and drive mechanism will drivethe central shaft in the mixing chamber.

A distinctive feature of the mixer and mixing method disclosed herein isthe ability of this mixer to blend reinforcing fibers with the rest ofthe cementitious components in a continuous operation without undulydamaging the added fibers. Furthermore, the mixer and mixing method ofthis invention allow production of a fiber reinforced cementitiousslurry mixture having a desirable working consistency. The fiber-slurrymixtures discharged from the multi-stage fiber-slurry mixer are suitablefor a variety of uses, for example statuary, shotcrete, consolidation ofloose rock, soil stabilization, pre-cast concrete products, pavement,repair application, or to make a fiber reinforced concrete buildingpanel or board. For instance, a workable slurry consistency facilitatesfurther processing and formation of panel products on a continuousforming line running at high line speeds.

The uniform fiber-slurry mixture produced has a consistency that willallow the fiber-slurry mixture to be discharged from the horizontalfiber-slurry mixer and be suitable for being deposited as a continuouslayer on a moving surface of a panel production line uniformly as alayer 0.25 to 2.00 inches thick, preferably 0.25 to 1 inches thick,typically 0.5 to 0.75 inches thick on the moving surface of the panelproduction line to produce a fiber reinforced concrete panel.

The multi-stage continuous mixer of this invention can either be adual-shaft mixer or a multi-shaft mixer. Preferably, the multi-stagecontinuous mixer of this invention is a dual-shaft mixer.

The multi-stage continuous mixer of this invention has an initial augersection and at least two mixing sections. The dry powders are introducedinto the mixer through an inlet port located at one end of the mixer.The augers located in the auger section move the dry powders forwardinto the first mixing section. The first mixing section is intended formixing the dry powders with the liquid additives including water toproduce a uniform blend of cementitious slurry mixture. The cementitiousslurry mixture so produced in the first section of the mixer is conveyedto the second mixer section. The second mixing section is where fibersare blended with cementitious slurry produced and conveyed from thefirst mixer section. The resultant fiber reinforced slurry mixture exitsthe mixer through an outlet port located at the end of the second mixersection.

The various key components and features of a multi-stage, dual-shaft (ormulti-shaft) continuous mixer disclosed as part of this invention can behighlighted as follows:

An Elongated Mixing Chamber

The elongated double barrel mixing chamber houses the dual rotatingshafts (or multi rotating shafts) of the continuous mixer.

The total length of the mixing chamber typically ranges from about 2 to8 feet. The preferred length of the mixing chamber is typically fromabout 3 to 6 feet.

The diameter of the mixing chamber typically ranges anywhere from about3 to 24 inches. The diameter of the mixing chamber preferably rangesfrom about 5 to 12 inches.

Dual rotating shafts (or multi rotating shafts) mounted in the elongatedmixing chamber traverse from one end of the mixer to another. The shaftsare externally connected to a drive mechanism and an electrical motor toaccomplish shaft rotation when the mixer is in operation. The shaftsrotate at a speed, ranging from 30 to 450 RPM, more preferably 40 to 300RPM, and most preferably 50 to 250 RPM. As part of the mixer developmentand optimization work, it has been discovered that relatively lowermixer speeds are preferable and provide excellent dispersion of fibersin the cementitious slurry mixture. Furthermore, another importantbenefit of using lower mixing speeds for the purposes of this inventionis that it results in reduced fiber breakage and superior materialworking properties useful in further processing of the fiber reinforcedcementitious slurry mixture. A variable frequency drive along withgearing, chain or a belt arrangement is typically used with the mixerfor turning the rotating shaft when the mixer is in operation. Thevariable frequency drive is helpful for adjusting and fine-tuning themixer speed for a given combination of raw materials involved in theproduction process.

An auger section is used to convey the dry powders from the mixer inletport to the first mixing section of the continuous mixer. The initiallength of the mixer shafts is in the form of an auger that accomplishesmovement of the dry powder forward. When dual-shafts (or multi-shafts)are used in the mixer, the individual shafts are positioned in the mixersuch that the flights from one auger section are in overlapping position(but non-interfering during shaft rotation) to the flights from thesecond auger section. This overlapping placement of the two augersections in the mixer provides self-cleaning action to the auger sectionof the mixer. The initial auger section (located near the dry powdermixer inlet) in a dual-shaft mixer configuration are shown in FIGS. 2Aand 2B.

FIG. 2A shows the horizontal dual shaft multi-stage continuousfiber-slurry mixer embodiment of the present fiber-slurry mixing device.In particular, FIG. 2A shows a first feed section 20 (also known as anauger section) having an auger 26 at the mixer inlet. FIG. 2A also showsa first mixing section 22 having flat paddles 25 mounted on the twoshafts.

FIG. 2B shows another view of the augers 26 in the first feed section 20(also known as an auger section) of the present fiber-slurry mixer 32.The length of first feed section 20 is typically from about 1 to 3 feet.The auger flight pitch may be varied depending upon the raw materialsused, raw material feed rates desired, and the design configuration ofthe two mixing sections of the mixer.

The first mixing section 20 comprises mixing paddles 25 mounted on theindividual rotating shafts of the mixer. There are two types of paddlesthat are typically used in the first mixing section—flat or helical.FIG. 2C shows a flat mixing paddle 25 as used in FIG. 2A. FIG. 2D showsa helical mixing paddle 27 that can be used in the first mixing sectionof this mixer. The flat paddles 25 provide a high shear mixing actionwith negligible conveying action to the material in the mixer. On theother hand, the helical paddles 27 provide both the mixing and (limited)conveying actions to the material in the mixer.

Flat paddles 25 and helical paddles 27 are unitary (one piece) paddleshaving a central opening fitted to the shaft such that the paddleencircles a portion of the shaft. Also, the flat paddles and helicalpaddles have opposed ends extending in opposite directions from theshaft. Flat paddles 25 and helical paddles 27 have a central hole withkey slots cut into them to allow the paddles to slide and mount onto akeyed shaft. The paddles are concentrically mounted and keyed on to theshaft. The orientation of the adjacent paddles mounted on the two shaftsof the dual shaft mixer is such that they provide wiping action withoutany rotational interference,

FIG. 2F shows flat paddles 25 and a helical paddle 27 on a shaft 29.Space 25A represents being filled by flat paddles 25 and/or helical 27paddles.

Other paddle shapes and geometries can also be used in the first mixingsection of the mixer. For example, of mixing and conveying paddles whicheach comprise a pin engaged to a paddle head can be employed in thefirst and/or second mixing sections as explained in more detail belowregarding FIG. 4A.

The paddles mounted on the individual shafts are in over-lapping butnon-interfering orientation when the mixer shafts are in rotational modeduring the mixer operation. FIGS. 2A and 2E show flat paddles 25 mountedon the two shafts (in the first mixing section) of a dual-shaft mixer.In particular, FIG. 2E shows an enlarged view of flat paddles 25 mountedon the two shafts in the first mixing section of the horizontal dualshaft multi-stage continuous fiber-slurry mixer embodiment of thepresent fiber-slurry mixing device. However, helical paddles 27 can besubstituted for some or all of the flat paddles 25.

The primary purpose of the paddles situated in the first mixing section22 of the mixer 32 is to blend the dry powder with the water and otherliquid additives (if any) to produce a uniform cementitious slurrymixture. Due to the over-lapping but non-interfering orientation of thepaddles, the rotation of the paddles 25 mounted on the individual shaftsprovides a self-cleaning action to the first mixing section 22 of themixer 32. The flat 25 or helical 27 mixing paddles mounted on the twoshafts are particularly useful in this regard. This provides excellentself-cleaning action due to the scraping action of the paddles againsteach other and against the barrel (shell) of the mixer. Flat paddles arethe most preferred paddles, as opposed to helical paddles, for use inthe first mixing section 22 for the purposes of this invention. Thelength of the first mixing section 22 is typically from about 1 to 4feet. More typically, the length of the first mixing section is about 3feet or less. The width of the individual flat or helical mixing paddlesranges from about 0.25″ to 4″. More typically, the width of the mixingflat or helical paddles is from 0.50″ to 3″. More typically, the widthof the mixing flat or helical paddles is from 1″ to 2″. The clearance ofthe mixing paddles, regardless of whether flat, or helical or anothershape, from the mixer shell is preferably less than ¼″, more preferablyless than ⅛″, and most preferably less than 1/16″.

The second mixing section 24 of the mixer 32 is where the reinforcingfibers are typically introduced into the mixer and blended with thecementitious slurry. The second mixing section 24 is essentially acontinuation of the first mixing section 22 and utilizes one or moremeans to blend fibers into the cementitious slurry. The reinforcingfibers through conduit 34 are introduced into the continuous mixer 32 atthe beginning of the second mixing section 24. The reinforcing fibersare blended with the cementitious slurry produced in the first mixingsection 22 using either mixing paddles or augers or a combinationthereof. The mixing paddles and/or augers are mounted on the dualrotating shafts of the mixer and help to blend the reinforcing fiberswith the cementitious slurry mixture conveyed from the first mixingsection. The mixing paddles (flat paddles 25 and/or helical paddles 27)as described and used in the first mixing section 22 may be used in thesecond mixing section 24 as well. However, use of such paddles has beenfound to cause significant fiber damage due to the high shear actionprovided by these paddles. Therefore, use of such paddles alone in thesecond mixing section is not preferred, particularly when a large numberof such paddles are used. Helical paddles are better suited than theflat paddles in the second mixing section to meet the objectives of thisinvention.

Augers can also be used for blending of fibers with the cementitiousslurry in the second mixing section 24. Augers used on their own providea rapid conveying action and a relatively less mixing action than thatprovided by the paddles alone. The augers mounted on the two parallelshafts in overlapping configuration further help with the self-cleaningaspect of the mixer.

Preferably if the flat paddles 25 or helical paddles 27 are employed inthe second mixing section 24 they are employed in a paddle portion ofthe second mixing section 24 and an auger is also employed in the secondmixing section 24 before and/or after the paddle section. A combinationof augers and a limited number of helical paddles (or less preferablyflat paddles) may also be used in the second mixing section 24. Suchcombination is in fact preferred and recommended for achieving bestmixing results for blending of fibers with the cementitious slurry. Theuse of a limited numbers of helical (or flat) paddles after the augersin the second mixing section 24 causes a resistance to the material flowthrough the mixer. This resistance to material flow provides for abetter mixing and wet-out of fibers with the cementitious slurry in thesecond mixing section of the mixer.

To summarize, the second mixing section 24 can be configured in one ormore ways as highlighted below to facilitate mixing of fibers with thecementitious slurry mixture:

FIG. 3A shows a first configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer 32 of the present invention with materialflow in the mixer in direction “X”. In the first configuration, augers26 are mounted on both impeller shafts 29 in the first feed section 20,mixing paddles are mounted on both impeller shafts 29 in the firstmixing section 22, and augers 29A only are mounted on both impellershafts 29 in the second mixing section 24. The auger parameters(example, auger pitch, auger length) are selected to maximize materialretention and promote a more intimate contact between the fibers and thecementitious slurry in the mixer 32. The total length of the secondmixing section and augers ranges from about 1 to 5 feet, more preferablyfrom about 2 to 4 feet. In this and other drawings of this specificationlike reference numbers in the drawings are intended to identify likeelements unless otherwise indicated.

FIG. 3B shows a second configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer 32 of the present invention with materialflow in the mixer in direction “X”. In the second configuration, augers29A followed by mixing/conveying paddles 29B mounted on both shafts 29in the second mixing section. Both flat paddles 25 or helical paddles 27may be used as mixing/conveying paddles 29B. The use of helical paddles7 is preferred in the second mixing section. The adjacent flat orhelical paddles mounted to a singular shaft in the second mixing sectioncan have the same orientation with respect to each other oralternatively they may be rotated with respect to each other. When theadjacent paddles on a shaft are rotated with respect to each other, theangle of rotation of the adjacent paddles may range from 0° to 90°,typically 20° to 90°. A greater number of paddles can be used in thesecond mixing section when the adjacent paddles have a zero degreerotation with respect to each other. Some of the helical paddles 27 usedmay also be placed in the reverse direction if desired to increase theresistance to material flow and fiber-slurry mixing action taking placein the augers 29A. When flat or helical paddles are used, the number ofpaddle sets (paddles per shaft) in the second mixing section 24preferably ranges 1 from 20, more preferably from 1 to 10. The paddleparameters (type, dimensions, orientation, number, and configuration)are selected to minimize the shearing action the material is subjectedto in the mixer 32. The paddles can be made of variety of materialsincluding metals, ceramics, plastics, rubber, or a combination thereof.Paddles with softer lining materials are also contemplated for use inthe second mixing section as they tend to minimize material and fiberdamage. Paddles with a pin and a head or only pins may alternatively beused in the second mixing section after the auger.

The auger parameters (example, auger pitch, auger length) are selectedto maximize material retention and promote a more intimate contactbetween the fibers and the cementitious slurry in the mixer 32. Thetotal length of the second mixing section ranges from about 1 to 5 feet,more preferably from about 2 to 4 feet. Only a small portion of thislength is taken up by the paddles 29B and a majority of the secondmixing section 24 is covered by the augers 29A.

FIG. 3C shows a third configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer 32 of the present invention with materialflow in the mixer in direction “X”. The third configuration has augers29A followed by mixing/conveying paddles 29B followed by augers 29Cmounted on both shafts 29 in the second mixing section. Both flatpaddles 25 or helical paddles 27 may be used as mixing/conveying paddles29B but the use of helical paddles 27 is preferred. Some of the helicalpaddles 27 used may also be placed in the reverse direction if desiredto increase the residence time and improve fiber-slurry mixing in theprevious auger section. The adjacent flat or helical paddles mounted toa singular shaft in the second mixing section can have the sameorientation with respect to each other or alternatively they may berotated with respect to each other. When the adjacent paddles on a shaftare rotated with respect to each other, the angle of rotation of theadjacent paddles may range from 0° to 90°, typically 20° to 90°. Whenflat or helical paddles are used, the number of paddle sets in thesecond mixing section 24 preferably ranges from 1 to 20 and morepreferably from 1 to 10. A greater number of paddles can be used in thesecond mixing section when the adjacent paddles have a zero degreerotation with respect to each other. The paddle parameters (type,dimensions, orientation, number, and configuration) are selected tominimize the shearing action the material is subjected to in the mixer32. Paddles with a pin and a head or only pins may alternatively be usedin the second mixing section after the auger. The auger parameters(example, auger pitch, auger length) are selected to maximize materialretention and promote a more intimate contact between the fibers and thecementitious slurry in the mixer. The total length of the second mixingsection ranges from about 1 to 5 feet, more preferably from about 2 to 4feet. Only a small portion of this length is taken up by the paddles anda majority of the second mixing section is covered by the augers.

FIG. 3D shows a fourth configuration of a dual-shaft multi-stagecontinuous fiber-slurry mixer 32 of the present invention with materialflow in the mixer in direction “X”. The fourth configuration hasmixing/conveying paddles 29D only mounted on both shafts 29 in thesecond mixing section of the mixer. The use of flat and helical paddlesin the second mixing section is not preferred in this configurationsince their use results in very high shear and causes significant fiberdamage. Mixing and conveying paddles that cause low mixing shear arepreferred when this mixer configuration is utilized in the second mixingsection. Use of paddles with a pin and a head or only pins is preferredin the second mixing section of this mixer configuration. However, inthis embodiment, it is acceptable to use any type of paddles, forexample flat and/or helical paddles, in the first mixing section.

FIG. 4A shows a drawing of an embodiment of the configuration(schematically shown in FIG. 3D) of the dual shaft (one shaft shown)fiber-slurry mixer 32 using such paddles 100 that cause low mixing shearin both the first mixing section 22 and the second mixing section 24.FIG. 4A shows the first feed section 20 having an auger 26, the shaft29, and paddles 100. The paddles 100 having a pin 114 and a broad paddlehead 116 that extends transverse relative to the pin 114. Preferably thefiber-slurry mixer 2 is a single shaft mixer.

FIG. 4A shows a powder mixture of, for example, Portland cement, gypsum,aggregate, fillers, etc. is fed from the dry powder feeder which istypically an overhead hopper bin 160A through a dry powder conduit 5A,which is a bellows 161, to an elongated horizontal mixing chamber 163 ofmixer 32. The impeller shaft 29 is driven by a side mounted impellermotor 172 that is regulated by a speed controller (not shown). Thepowder mixture solids may be fed from the hopper bin 160A to thehorizontal mixing chamber 163 containing the auger 26 by a volumetricfeeder or a gravimetric feeder (not shown).

Volumetric feeding systems would use an auger screw conveyor (not shown)running at a constant speed to discharge powder from the storage hopperbin 160A at a constant rate (volume per unit time, e.g., cubic feet perminute). Gravimetric feeding systems generally use a volumetric feederassociated with a weighing system to control the discharge of powderfrom the storage hopper bin 160A at a constant weight per unit of time,e.g., pounds per minute. The weight signal is used via a feedbackcontrol system to constantly monitor the actual feed rate and compensatefor variations in bulk density, porosity, etc. by adjusting the speed(RPM) of the auger screw of the auger screw feeder. Such volumetricfeeding systems can also be used for any other embodiments of the mixer32.

Aqueous medium, such as water, from a liquid pump (not shown) feeds thehorizontal chamber 163 through a nozzle of at least one aqueous mediumstream conduit 7A.

FIG. 4A shows the elongated horizontal mixing chamber 163 comprisescylindrical horizontal sidewalls 102, a first end wall 104, and a secondend wall 106. Material flow is in a direction X from the first end wall104 to the second end wall 106. Shaft 29 extends from first end wall 104to second end wall 106. The horizontal fiber-cementitious slurry mixer32 also comprises at least one rotatable shaft 29 (preferably tworotatable shafts, wherein the second shaft is not shown for clarity), anaqueous liquid medium conduit 7A for feeding liquid comprising waterinto the chamber 163, a reinforcement fiber conduit 34A for feedingreinforcement fiber into the chamber 163, and a fiber-slurry mixturedischarge outlet 36A for discharging fiber-slurry mixture. Mixing andconveying paddles 100 extend from the central rotatable shaft 29. Thehorizontal fiber-cementitious slurry mixer 32 also comprises other inletports 167, one shown, to feed other raw materials and performanceenhancing additives into the mixer 32. The horizontal fiber-cementitiousslurry mixer 32 also comprises a venting port 70 to remove any airintroduced into the mixing chamber 163 from raw material feed. Thehorizontal fiber-cementitious slurry mixer 32 also comprises anelectrical motor and drive mechanism 172 to drive the central shaft 29in the mixing chamber 163.

The rotatable shaft 29 rotates about its longitudinal axis “A” to mixthe fed ingredients and convey them as fiber-slurry mixture to thedischarge outlet 168. The rotatable shaft has the auger 26 in thechamber first feed section 20, and paddles 100 in both the first mixingsection 22 and the second mixing section 24.

The reinforcement fibers and cementitious slurry and other ingredientswill be fed to the mixer 32 at respective rates to leave an open spacein the mixer above resulting mixture to facilitate mixing and conveying.If desired, a liquid level control sensor is used to measure the levelof the slurry in the horizontal chamber of the mixer.

The rotatable shaft 29 may include a first end assembly 160 and a secondend assembly 162. First end assembly 160 and second end assembly 162 maytake any of a wide variety of forms known to one of skill in the art.For example, first end assembly 160 may include a first end engagementportion that operatively engages a first end of the rotatable shaft 29,a first cylindrical portion 164 extending from the first end engagementportion, an intermediate cylindrical portion 166 extending from thefirst cylindrical portion 164, and an end cylindrical portion 168,extending from the intermediate cylindrical portion 166 and including aslot 170. The second end assembly 162 may include a second endengagement portion that operatively engages a second end of therotatable shaft 29, a first cylindrical portion 165 extending from thesecond end engagement portion, and an end cylindrical portion 169extending from the first cylindrical portion. In at least oneembodiment, first end engagement portion of first end assembly 160 maybe engaged to the rotatable shaft 29 proximate to first cylindricalproportion 164. In one or more embodiments, end cylindrical portion 168may be operatively engaged to a motor 172 or engine capable of impartingrotation (e.g., high-speed rotation) to rotatable shaft 29 and the oneor more paddle assemblies 100 engaged therewith to mix the reinforcementfibers and cementitious slurry. In at least one embodiment, second endengagement portion of second end assembly 162 may be engaged to a secondend (e.g., an end opposing the first end) of rotatable shaft 29proximate to first cylindrical portion 165. In one or more embodiments,end cylindrical portion 169 of second end assembly 162 may be preferablyengaged to a bearing assembly, which may be integral to an exterior wallof the horizontal fiber-cementitious slurry mixer 32, to permit therotation of rotatable shaft 29.

As seen in FIG. 4A, a plurality of paddle assemblies 100 may bepermanently and/or removably engaged (e.g., affixed, adhered, connected,etc.) to rotatable shaft 29 and configured into, for example, alignedrows and/or columns (e.g., rows along the length of the rotatable shaft29, columns around the circumference of the rotatable shaft 29. In oneor more embodiments, paddle assemblies 100 may be permanently orreleasably engaged to rotatable shaft 29 in offset rows or columns asdesired. In addition, rotating shaft 29 may accommodate any arrangementor configuration of paddle assemblies 100 as desired, preferably but notlimited to spiral and/or helical configurations.

The rotatable shaft 29, in one or more embodiments, may be constructedto rotate at a predetermined rate 30 to 450 RPM, more preferably 40 to300 RPM, and most preferably 50 to 250 RPM during mixing

Paddle pin 114 has a width W1 which is less than a width W2 of paddlehead 116 (See FIG. 4B). Pin 114 of mixing and conveying paddle 100 mayinclude a threaded end portion 115 (See FIG. 4B) adapted for engagementinto a threaded opening of the rotatable shaft 29, such that mixing andconveying paddle 100 may be rotated to achieve a desired or selectedpitch (e.g., angle) relative to the rotatable shaft 29. In one or moreembodiments, each mixing and conveying paddle 100 may be rotated adesired distance into the rotatable shaft 29, wherein the distance maybe the same or different from one or more other paddle assemblies orsections of paddle assembles as engaged to the rotatable shaft 29. Thepaddles may be attached to the central shaft using different meansincluding threaded attachment (as shown) and/or welding attachment (notshown).

FIG. 4E shows a configuration (schematically shown in FIG. 3B) of adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixer32 in which the first mixing section 22 has paddles 100 and the secondmixing section 24 has augers 29A followed by paddles 100 on both shafts29.

FIG. 4F shows a configuration (schematically shown in FIG. 3C) of adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixer32 in which augers 26 are mounted on both impeller shafts 29 in the feedsection 20, the first mixing section 22 has paddles 100 and the secondmixing section 24 has an auger 29A followed by paddles 100 followed byan auger 29C on both shafts 29.

FIG. 4G shows a configuration (schematically shown in FIG. 3C) of adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixer32 in which augers 26 are mounted on both impeller shafts 29 in the feedsection 20, the first mixing section 22 has paddles 100 and the secondmixing section 24 has the auger 29A followed by pin/s 114 followed bythe auger 29C on both shafts 29.

FIG. 4H shows a configuration (schematically shown in FIG. 3D) of thehorizontal dual-shaft (one shaft shown) multi-stage continuousfiber-slurry mixer 32 in which augers 26 are mounted on both impellershafts 29 in the feed section 20, the first mixing section 22 haspaddles 100 and second mixing section 24 has only pins 114 on bothshafts 29.

FIG. 4I shows a configuration (schematically shown in FIG. 3A) having adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixer32 of the present invention in which augers 26 are mounted on bothimpeller shafts 29 in the feed section 20, the first mixing section 22has paddles 25, 27 and the second mixing section 24 has augers 29A onboth shafts), wherein the paddles are flat paddles 25 and/or helicalpaddles 27.

FIG. 4J shows a diagrammatic elevational side view of the configuration(schematically shown in FIG. 3B) having a dual-shaft (one shaft shown)multi-stage continuous fiber-slurry mixer of the present invention inwhich augers 26 are mounted on both impeller shafts 29 in the feedsection 20, the first mixing section 22 has paddles 25, 27 and thesecond mixing section 24 has augers 29A followed by paddles 25, 27 onboth shafts, wherein the paddles are flat paddles 25 and/or helicalpaddles 27. The empty space 25A between paddles where the shaft 29 isvisible is intended to convey presence of paddles. In this mixerconfiguration, the adjacent paddles of the second mixing section on ashaft may be rotated with respect to each other or they may have a zerodegree rotation with respect to each other, i.e. the paddles areuniformly aligned with respect to each other.

FIG. 4K shows a configuration (schematically shown in FIG. 3C) in whichaugers 26 are mounted on both impeller shafts 29 in the feed section 20,the first mixing section 22 has flat paddles 25 and/or helical paddles27 and the second mixing section has an auger 29A followed by flatpaddles 25 and/or helical paddles 27 followed by an auger 29C on bothshafts (one shaft shown for clarity). The empty space 25A betweenpaddles where the shaft 29 is visible is intended to convey presence ofpaddles.

FIG. 4L shows a configuration (schematically shown in FIG. 3D) having adual-shaft (one shaft shown) multi-stage continuous fiber-slurry mixer32 of the present invention in which augers 26 are mounted on bothimpeller shafts 29 in the feed section 20, the first mixing section 22has paddles and the second mixing section 24 has paddles on both shafts29, wherein the paddles are flat paddles 25 or helical paddles 27. Theempty space 25A where the shaft 29 is visible is intended to conveypresence of paddles. In this mixer configuration, it is preferred thatthe adjacent paddles of the second mixing section on a shaft have a zerodegree rotation with respect to each other, i.e. the paddles areuniformly aligned with respect to each other,

FIG. 4M shows a variation of the configuration (schematically shown inFIG. 3A) having a dual-shaft (one shaft shown) multi-stage continuousfiber-slurry mixer 32 of the present invention in which augers 26 aremounted on both impeller shafts 29 in the feed section 20, first mixingsection 22 can have one type of paddles and the second mixing section 24can have a different type of paddles. The preferred arrangement in thisconfiguration is to have flat paddles 25 and/or helical 27 paddles inthe first mixing section 22 and paddles 100 with a pin 114 and a head116 and/or only pins 114, in the second mixing section 24. Mostpreferably the paddles in the first mixing section are flat or helical,and paddles in the second mixing section comprise paddles with a pin anda head and/or pins.

In the mixer configurations of the invention employing flat and/orhelical paddles in the second mixing section, for example in the mixersof FIGS. 4I, 4J, 4K, 4L, and 4M, the flat paddles 25 and/or helicalpaddles 27 are on the shaft 29; and all adjacent flat and/or helicalpaddles on the shaft 29 in the second mixing section 24 have a 0 to 90degree rotation with respect to each other.

If desired the flat and/or helical paddles are on the shaft in thesecond mixing section and all adjacent flat and/or helical paddles onthe shaft in the second mixing section have a zero degree rotation withrespect to each other.

If desired the flat and/or helical paddles are on the shaft in thesecond mixing section and all adjacent flat and/or helical paddles onthe shaft in the second mixing section have a 30 degree rotation withrespect to each other.

If desired the flat and/or helical paddles are on the shaft in thesecond mixing section and all adjacent flat and/or helical paddles onthe shaft in the second mixing section have a 45 degree rotation withrespect to each other.

If desired the flat and/or helical paddles are on the shaft in thesecond mixing section and all adjacent flat and/or helical paddles onthe shaft in the second mixing section have a 60 degree rotation withrespect to each other.

If desired the flat and/or helical paddles are on the shaft in thesecond mixing section and all adjacent flat and/or helical paddles onthe shaft in the second mixing section have a 90 degree rotation withrespect to each other.

The above mentioned features and parameters of the fiber-slurrycontinuous mixer of this invention are further described as follows.This applies not only to the embodiments of the drawings but theinvention in general unless otherwise indicated.

Elongated Mixing Chamber

The elongated mixing chamber is typically cylindrical in shape. Thelength of the mixing chamber typically ranges anywhere from about 2 to 8feet. The preferred length of the mixing chamber is from about 3 to 5feet. The diameter of the mixing chamber typically ranges anywhere fromabout 4 to 24 inches. The preferred diameter of the mixing chamberranges from about 6 to 12 inches.

Rotating Shafts

The diameter of each of the dual or multi-rotating shafts is typicallyfrom about 1 to 4 inches. The preferred diameter of the central shaftsranges from about 1 to 3 inches.

The central rotating shafts rotate at a speed, preferably ranging fromabout 30 to 450 RPM, more preferably 40 to 300 RPM, and most preferably50 to 250 RPM. It has been discovered that relatively lower mixer speedsare preferable to meet the objectives of the present invention. It hasbeen surprisingly found that excellent fiber dispersion in thecementitious slurry mixture can be obtained even at relatively low mixerspeeds. Furthermore, another important benefit of using lower mixingspeeds is that it results in reduced fiber breakage and superiormaterial working and flow properties useful in further processing of thefiber reinforced cementitious slurry mixture.

A variable frequency drive is preferably used with the mixer for turningthe central rotating shaft when the mixer is in operational mode. Thevariable frequency drive is helpful for adjusting and fine-tuning themixer speed for a given combination of raw materials involved in theproduction process.

The continuous mixers of the present invention can either be asingle-shaft mixer, a dual-shaft mixer, or a multi-shaft mixer. Thisdisclosure describes the dual-shaft mixers of the present invention ingreater detail. However, it is contemplated that single-shaft ormultiple-shaft mixers in accordance to the present invention can also bebeneficially employed for producing fiber reinforced cementitious slurrymixtures possessing desirable properties that are useful in a variety ofapplications including continuous production processes.

Mixing Paddles

The mixing paddles mounted on the central shaft can have differentshapes and dimensions to facilitate mixing and conveying of the addedcomponents in the mixer.

As explained above the invention may employ flat paddles and helicalpaddles.

The mixing paddles suitable for use in the present invention alsoinclude paddles with a pin and a relatively wider head to help move thematerial forward, for example paddle 100. In addition to the paddleshaving one type of pin and head, the fiber-slurry mixer may include morethan one type of paddle having a pin and a relatively wider head, orjust pins, to achieve desirable characteristics required for furtherprocessing of the material. However, as seen in FIG. 4B the inventionmay employ a single style paddle in both the first mixing section 22 andsecond mixing section 24. However, use of flat or helical paddles ismost preferred in the first mixing section of the fourth mixerconfiguration which has paddles in both the first mixing section 22 andthe second mixing section 24. Further, use of paddles 100 with a pin 114and a head 116 or only pins 114 is most preferred in the second mixingsection 24 of the fourth mixer configuration. The use of the same typeof paddles in both mixing sections is allowed in the fourth mixerconfiguration but is not preferred.

The overall dimensions of the paddles are such that the clearance(space) between the inner circumference of the mixer chamber and thepaddle's furthermost point from the central shaft is preferably lessthan ¼″, more preferably less than ⅛″, and most preferably less than1/16″. Too great a distance between the paddle tips and the inner wallsof the chamber would result in slurry build-up. Pins 114 can besubstituted for at least some of the paddles 100. For example, the pinsmay be the pins 114 of the paddles 100 without the broad paddle head116.

The quality of mixing and conveying of the components in the mixer isalso dictated by the orientation of the paddles in the mixer. A parallelor perpendicular paddle orientation with respect to the cross-section ofthe central shaft diminishes the conveying action of the paddles thusincreasing the residence time of the material in the mixer. An increasedresidence time of the material in the mixer can lead to significantfiber damage and production of fiber reinforced cementitious slurrymixture having undesirable characteristics. When employing paddleshaving pins and heads, for example paddle 100, the orientation of thelongitudinal axis “LH” of the paddle head 116 with respect to thelongitudinal axis “A” of the central shaft 118 is preferably at an angle“B” (FIG. 4C) from about 10° to 80°, more preferably from about 15° to70°, and most preferably from about 20° to 60°. The use of preferredpaddle orientation leads to a more efficient mixing and conveying actionof the slurry mixture and causes minimal damage to the reinforcingfibers in the mixer.

FIG. 4D provides a close-up view of the mixer 32 with a door 37 to themixing chamber 163 open showing the orientation of the paddles 100 withrespect to the central shaft 29 (one shaft shown). Placement of thepaddles 100 on the central shaft 118 in the spiral form can also beobserved.

When employing paddles having pins and heads, for example paddle 100,the set of paddles in the mixer are typically configured in a spiralform on the central shaft from one end of the mixer to another. Thisarrangement of paddles further facilitates conveying action of thematerial inside the mixer. Other configurations of paddle arrangement inthe mixer are possible and are contemplated as part of this invention.

The paddles can be made of variety of materials including metals,ceramics, plastics, rubber, or a combination thereof. Paddles withsofter lining (coating) materials are also contemplated as they tend tominimize material and fiber breakage.

The paddles and/or inner walls of the elongated mixing chamber may becoated with a release material, to minimize buildup of the cementitiousslurry on the paddles and/or shell.

Other Configurations:

Other combinations of augers and mixing/conveying paddles to achieve theobjectives of this invention are possible and contemplated as part ofthis invention. When employing paddles having pins and heads, forexample paddle 100, these types of paddles may be used on their own inthe first mixing section 22 and second mixing section 24 as describedabove and shown in FIG. 4B or they may be used in combination withaugers. For example, paddles having pins and heads, for example paddle100, may be employed to substitute for the paddles 29B in FIGS. 3B-3C.

Inlet Ports

The inlet conduits 5A, 7A, 34A for the raw materials, such as the drycementitious powder, aqueous liquid medium, and fibers fees into themixer at inlet ports of the mixing chamber. The size, location, andorientation of raw material inlets ports of the fiber-slurry mixer areconfigured to ease introduction of the raw material into the mixer andto minimize potential for blocking of ports from the slurry mixture inthe mixer.

The continuous fiber-slurry mixer has at least one inlet port tointroduce dry powders into the mixing chamber. This inlet port islocated at the beginning of the first feed section (auger section) ofthe continuous fiber-slurry mixer.

The continuous fiber-slurry mixer has at least one inlet port tointroduce aqueous medium comprising water into the mixing chamber. Thewater inlet port is typically located at the end of the first feedsection (auger section) of the continuous fiber-slurry mixer. Thecontinuous fiber-slurry mixer can have additional inlet ports tointroduce other performance enhancing additives into the mixing chamber.These inlet ports are typically located at the end of the auger sectionor the beginning of the first mixing section of the co continuousfiber-slurry.

The continuous fiber-slurry mixer has at least one inlet port tointroduce reinforcing fibers into the mixing chamber. The fiber inletport is typically located at the beginning of the second mixing sectionof the continuous fiber-slurry mixer. The fibers can be introduced intothe continuous fiber-slurry mixer gravimetrically or volumetricallyusing a variety of metering equipment such as screw feeders or vibratoryfeeders. Fibers can be conveyed from a fiber feeder to the fiber-slurrymixer by a variety of conveying devices. For example, fibers can betransferred using screws (augers), air conveying, or simple gravitydeposition. The discrete or chopped fibers can be made of differentreinforcing fiber materials including fiberglass; polymeric materialssuch as polypropylene, polyethylene, polyvinyl alcohol, etc; carbon;graphite; aramid; ceramic; steel; cellulosic, paper, or natural fiberssuch as jute or sisal; or a combination thereof. Preferably the fibersare fiberglass. The fiber length is about 2 inches or lower, morepreferably 1.5 inches or lower and most preferably 0.75 inches or lower.

The continuous fiber-slurry mixer has an outlet port to discharge thefiber reinforced cementitious slurry mixture produced by the continuousfiber-slurry mixer. The outlet port is located at the end of the secondmixing section of the continuous fiber-slurry mixer.

The mixer has a venting port to remove any air introduced into themixing chamber from raw material feed.

An electrical motor and drive mechanism to drive the shafts areassociated with the mixing chamber.

Panel Production

Fiber reinforced cementitious slurry made using this mixer can be usedfor a variety of other applications. One of the uses of the fiber-slurrymixture is in panel production. In particular, production of fiberreinforced structural concrete panels is one preferred use.

Referring now to FIGS. 5 and 6, a cementitious panel production line forproducing fiber reinforced concrete (FRC) panels is diagrammaticallyshown and is generally designated 10. The production line 10 includes asupport frame or forming table 12 having a plurality of legs 13 or othersupports. Included on the support frame 12 is a moving carrier 14, suchas an endless rubber-like conveyor belt with a smooth, water-impervioussurface, however porous surfaces are contemplated. As is well known inthe art, the support frame 12 may be made of at least one table-likesegment, which may include designated legs 13 or other supportstructure. The support frame 12 also includes a main drive roll 16 at adistal end 18 of the frame, and an idler roll 17 at a proximal end 19 ofthe frame. Also, at least one belt tracking and/or tensioning device 15is typically provided for maintaining a desired tension and positioningof the carrier 14 upon the rolls 16, 17. In this embodiment, thecementitious panels (FRC panels) are produced continuously as the movingcarrier proceeds in a direction “T” from the proximal end 19 to thedistal end 18.

In this embodiment, a web 61 of release paper, polymer film or a plasticcarrier, or nonwoven fiber mats for supporting a slurry prior tosetting, may be provided and laid upon the carrier 14 to protect itand/or keep it clean. However, it is also contemplated that, rather thanthe continuous web 61, individual sheets (not shown) of a relativelyrigid material, e.g., sheets of polymer plastic, may be placed on thecarrier 14. These carrier films or sheets may be removed from theproduced panels at the end of the line or they may be incorporated as apermanent feature in the panel as part of the overall composite design.When these films or sheets are incorporated as a permanent feature inthe panel they may provide enhanced attributes to the panel includingimproved aesthetics, enhanced tensile and flexural strengths, enhancedimpact and blast resistance, enhanced environmental durability such asresistance to water and water vapor transmission, freeze-thawresistance, salt-scaling resistance, and chemical resistance.

Optionally a layer of discrete reinforcing fibers (not shown) may bedeposited directly on the conveying belt (carrier), release paper, orforming sheet upstream of the headbox 40.

In this embodiment, continuous reinforcement 44 such as a roving or aweb of reinforcing scrim such as fiberglass scrim or a nonwoven fibermat such as nonwoven fiberglass mat or a nonwoven polypropylene mat maybe provided for embedding in the slurry prior to setting and reinforcingthe resulting cementitious panels. The continuous rovings and/orreinforcing scrim roll 42 are fed through the headbox 40 to be laid uponthe carrier 14. However, it is also contemplated that, the continuousreinforcement 44 not be employed. The continuous scrim, nonwoven fabric,or rovings can be made of different reinforcing fiber materialsincluding fiberglass; polymeric materials such as polypropylene,polyethylene, polyvinyl alcohol, etc.; carbon; graphite; aramid;ceramic; steel; cellulosic or natural fibers such as jute or sisal; or acombination thereof. A roving is an assemblage of continuous reinforcingmonofilaments. Scrim is a web of continuous fibers running in themachine direction and the cross-direction. Reinforcement may also beprovided as a non-woven web made of discrete reinforcement fibers.

It is also contemplated that the cementitious panels produced by thepresent line 10 are formed directly upon the carrier 14. In the lattersituation, at least one belt washing unit 28 is provided. The carrier 14is moved along the support frame 12 by a combination of motors, pulleys,belts or chains which drive the main drive roll 16 as is known in theart. It is contemplated that the speed of the carrier 14 may vary tosuit the product being made.

The present production line 10 includes the continuous multi-stagefiber-slurry mixer 32 described above. The fiber-slurry mixer 32 may bea dual shaft or multi-shaft mixer. Dry powder feeder 2 feeds drycomponents 5 of the cementitious composition, except for reinforcingfibers, to the feed section 20 of the multi-stage continuous slurrymixer 32. Liquid pump 3 feeds aqueous medium 7, such as water, withliquid or water soluble additives to the first mixing section 22 of themixer 32. The first mixing section 22 of the multi-stage continuousmixer 32 mixes the dry components and the aqueous medium to form acementitious slurry. The cementitious slurry feeds the second mixingsection 24 of the mixer 32. Also, fiber feeder 33 feeds fibers 34 to thefiber-slurry mixer 32. Thus, in the second mixing section 24 of themixer 32 the fibers and cementitious slurry are mixed to form afiber-slurry mixture 36. The fiber-slurry mixture 36 feeds a headbox 40.

Headbox 40 (or other type of slurry distributor) deposits thefiber-slurry mixture on the web 26 of release paper (if present)traveling on the moving carrier 14. Continuous reinforcement in form ofrovings or scrim or nonwoven fabric may be deposited on either one orboth surface of the panel. If desired, continuous reinforcement 44provided by fiber rovings or spools and/or scrim roll 42 is also passedthrough the headbox 40 as shown in FIG. 6 to deposit on top of thedeposited fiber-slurry mixture 46. To assist in leveling thefiber-slurry mixture 46 a forming vibrating plate 50 may be providedunder or slightly downstream of the location where the headbox 40deposits the fiber-slurry mixture 46.

The fiber-slurry mixture 46 sets as it travels along the moving carrier14. To assist in leveling the fiber-slurry mixture 46 as it is settingthe fiber-slurry mixture 46 passes under one or more vibrating screedplates 52. At the distal end 18 of the support frame 12 a cutter 54 cutsthe set fiber-slurry mixture into boards 55. The boards (panels) 55 arethen placed on an unloading and curing rack 57 (See FIG. 6) and allowedto cure.

Optionally, rather than applying scrim or rovings or nonwoven fabric 44from roll 42 to the top of the deposited fiber-slurry mixture 46,discrete reinforcing fibers (not shown) may be deposited on the surfaceof the fiber-slurry mixture 46 between the headbox 40 and the firstscreed plate 52. The deposited fibers are then embedded by the screedplates 52. Such bottom continuous reinforcement, if desired, is fedbehind the headbox 40 and it rests directly on top of theconveying/forming belt. The bottom continuous reinforcement passes underthe headbox and the slurry in the headbox 40 is poured directly on itstop as the continuous reinforcement moves forward. For example,continuous reinforcement can be provided by web 26 or a roll (not shown)upstream to the headbox in addition to that providing web 26 to lay thecontinuous reinforcement above web 26.

FIG. 6 further shows edge formation and leakage prevention devices 80.These are edge belts or edge rails (used singly or in combination).

The fiber-cement mixtures produced by this invention contain cement,water, and other cement additives. However, to achieve the desiredviscosity the cementitious compositions preferably avoid thickeners orother high viscosity processing aids at high dosage rates as commonlyused with fiber cement extrusion. For example, the present slurriespreferably avoid high viscosity cellulose ethers at high dosage rates.Examples of high viscosity cellulose ethers which the present slurriesavoid are methyl cellulose, hydroxypropyl methyl cellulose, andhydroxyethyl methylcellulose.

The fiber-cement mixtures produced by this invention are aqueousslurries which may be made by adding fibers to a variety of settablecementitious slurries. For example, compositions based on hydrauliccements or based on gypsum. ASTM defines “hydraulic cement” as follows:a cement that sets and hardens by chemical interaction with water and iscapable of doing so under water. Examples of suitable hydraulic cementsare Portland cement, calcium aluminate cements (CAC), calciumsulfoaluminate cements (CSA), geopolymers, magnesium oxychloride cements(sorel cements), and magnesium phosphate cements. A preferred geopolymeris based on chemical activation of Class C fly ash.

While calcium sulfate hemihydrate (gypsum) sets and hardens by chemicalinteraction with water, it is not included within the broad definitionof hydraulic cements in the context of this invention. However, calciumsulfate hemihydrate may be included in fiber-cement mixtures producedusing this invention. Thus, also such aqueous slurries may be based oncalcium sulfate cements such as gypsum cements or plaster of Paris.Gypsum cements are primarily calcined gypsum (calcium sulfatehemihydrate). It is customary in the industry to term calcined gypsumcements as gypsum cements.

The fiber-cement mixtures contain sufficient water to achieve thedesired slump test value and viscosity in combination with the otheringredients of the fiber-cement mixtures. If desired the composition mayhave a weight ratio of water-to-reactive powder of 0.20/1 to 0.90/1,preferably 0.20/1 to 0.70/1.

The fiber-cement mixtures may contain pozzolanic material such as silicafume, a finely divided amorphous silica which is the product of siliconmetal and ferro-silicon alloy manufacture. Characteristically, it hasvery high silica content and low alumina content. Various other naturaland man-made materials have been referred to as having pozzolanicproperties, including pumice, perlite, diatomaceous earth, tuff, trass,metakaolin, microsilica, and ground granulated blast furnace slag. Flyash also has pozzolanic properties. The fiber-cement mixtures maycontain Ceramic microspheres and/or Polymer microspheres.

However, one preferred use of the fiber-cement slurries made by thepresent method is to produce FRC panels suitable as structural cementpanels (SCP panels) having reinforcing fibers such as fiberglass,particularly alkali resistant glass fibers. As such, the cementitiousslurry is preferably comprised of varying amounts of Portland cement,gypsum, aggregate, water, accelerators, plasticizers, superplasticizers,foaming agents, fillers and/or other ingredients well known in the art,and described in the patents listed below which have been incorporatedby reference. The relative amounts of these ingredients, including theelimination of some of the above or the addition of others, may vary tosuit the intended use of the final product.

Water reducing admixture additives optionally can be included in thefiber-cement mixture, such as, for example, plasticizers andsuperplasticizers and dispersants, to improve the fluidity of ahydraulic slurry. Such additives disperse the molecules in solution sothey move more easily relative to each other, thereby improving theflowability of the entire slurry. Sulfonated melamines and sulfonatednaphthalenes, and polycarboxylate based superplasticizers can be used assuperplasticizers. Water reducing admixture additive can be present inan amount from 0% to 5%, preferably 0.5 to 5%, by weight of the wetfinish fiber-slurry mixture.

U.S. Pat. No. 6,620,487 to Tonyan et al., incorporated herein byreference in its entirety, discloses a reinforced, lightweight,dimensionally stable structural cement panel (SCP) which employs a coreof a continuous phase resulting from the curing of an aqueous mixture ofcalcium sulfate alpha hemihydrate, hydraulic cement, an active pozzolanand lime. The continuous phase is reinforced with alkali-resistant glassfibers and containing ceramic microspheres, or a blend of ceramic andpolymer microspheres, or being formed from an aqueous mixture having aweight ratio of water-to-reactive powder of 0.6/1 to 0.7/1 or acombination thereof. At least one outer surface of the SCP panels mayinclude a cured continuous phase reinforced with glass fibers andcontaining sufficient polymer spheres to improve nailability or madewith a water-to-reactive powders ratio to provide an effect similar topolymer spheres, or a combination thereof.

If desired the composition may have a weight ratio of water-to-reactivepowder of 0.2/1 to 0.7/1.

Various formulations for the composite slurry used in the currentprocess are also shown in published US applications US2006/0185267,US2006/0174572; US2006/0168906 and US 2006/0144005, all of which areincorporated herein by reference in their entirety. A typicalformulation would comprise as the reactive powder, on a dry basis, 35 to75 wt. % (typically 45-65 or 55 to 65 wt. %) calcium sulfate alphahemihydrate, 20 to 55 wt. % (typically 25-40 wt. %) hydraulic cementsuch as Portland cement, 0.2 to 3.5 wt. % lime, and 5 to 25 wt. %(typically 10-15 wt. %) of an active pozzolan. The continuous phase ofthe panel would be uniformly reinforced with alkali-resistant glassfibers and would contain 20-50% by weight of uniformly distributedlightweight filler particles selected from the group consisting ofceramic microspheres, glass microspheres, fly ash cenospheres andperlite. An example of a formulation for the composite slurry includesfrom 42 to 68 wt. % reactive powders, 23 to 43 wt. % ceramicmicrospheres, 0.2 to 1.0 wt. % polymer microspheres, and 5 to 15 wt. %alkali-resistant glass fibers, based on the total dry ingredients.

U.S. Pat. No. 8,038,790 to Dubey et al, incorporated herein byreference, provides another example of a preferred formulation for thecomposite slurry which includes an aqueous mixture of a cementitiouscomposition comprising, on a dry basis, 50 to 95 wt % reactive powder, 1to 20 wt % of coated hydrophobic expanded perlite particles uniformlydistributed as lightweight filler therein, the coated hydrophobicperlite particles having a diameter in the range of about 1 to 500microns (micrometers), a median diameter of 20 to 150 microns(micrometers) and an effective particle density (specific gravity) ofless than about 0.50 g/cc, 0 to 25 wt % hollow ceramic microspheres, and3 to 16 wt. % alkali-resistant glass fibers for uniformly distributedfor reinforcement; wherein the reactive powder comprises: 25 to 75 wt. %calcium sulfate alpha hemihydrate, 10 to 75 wt. % hydraulic cementcomprising Portland cement, 0 to 3.5 wt. % lime, and 5 to 30 wt. % of anactive pozzolan; and the panel having a density of 50 to 100 pounds percubic foot.

Although the above compositions for the composite fiber-slurry mixtureare preferred, the relative amounts of these ingredients, including theelimination of some of the above or the addition of others, may vary tosuit the intended use of the final product.

Slurry Feed Apparatus (Headbox)

Referring now to FIG. 5 a fiber-slurry feeder (also known as afiber-slurry headbox 40) receives a supply of fiber-slurry mixture 36from the fiber-slurry mixer 32.

The headbox 40 is disposed transversely to the direction of travel “T”of the carrier 14. The fiber-slurry mixture 36 is deposited in a cavityof the headbox 40 and discharges as fiber-slurry mixture stream 46through a discharge opening of the headbox 40 onto the moving carrierweb 14 (conveyor belt).

The fiber reinforced cementitious slurry can be pumped through a hoseand hose oscillator system into the headbox 40 or it may be dropped viagravity into the headbox 40 directly from the fiber-slurry mixer 32. Theoscillator system would be used in either case to agitate the slurry.Thickness of the product formed using the headbox 40 is controlled bythe slurry flow rate in the headbox 40, the amount of slurry elevationhead in the headbox 40, and headbox discharge opening gap for a givenline speed. The discharge opening gap of the headbox 40 is a transverseopening through which the fiber-slurry mixture discharges from theheadbox 40 onto the moving carrier web 14. The fiber-slurry mixture fromthe headbox deposits onto the moving carrier 14 in one step at close tothe desired thickness and finish of the final panel 55. Vibration may beadded to improve formation. Also, different forms of continuousreinforcements such as scrims and rovings may be added to improveflexural strength of the formed product. For example, a vibration unit50 may be located below the headbox 40 under the conveyor belt 14.

The vibration unit 50 is typically a single mass system of a table,springs, and two motors which direct forces directly into the depositedmat of fiber-cement slurry and cancel out in other directions. This unit50 is placed under the headbox 40 and it extends about 3 to 6 inchesbeyond the head box.

The headbox 40 deposits an even layer of the fiber-slurry mixture 46 ofrelatively controlled thickness upon the moving carrier web 14. Suitablelayer thicknesses range from about 0.25 inch to 2 inches, preferably 0.4to 0.8 inches thick.

The fiber-slurry mixture 46 is completely deposited as a continuoussheet of slurry uniformly directed down to within a distance of about1.0 to about 1.5 inches (2.54 to 3.81 cm.) of the carrier web 14.

As the fiber-slurry mixture 46 moves toward the moving carrier web 14,it is important that all of the slurry be deposited on the carrier web14.

Forming and Smoothing and Cutting

Upon the disposition of the layer of fiber-embedded settable slurry asdescribed above, the frame 12 may have forming devices provided to shapean upper surface of the setting slurry-fiber mixture 46 traveling on thebelt 14.

In addition to the above-mentioned vibrating table (forming andvibrating plate) 50 that assists to smooth the slurry being deposited bythe headbox 40, the production line 10 may include smoothing devices,also termed vibrating screed plates 52, to gently smooth the uppersurface of the panel (see FIGS. 5 and 6).

By applying vibration to the slurry 46, the smoothing device 144facilitates the distribution of the fibers 34 throughout the panel 55,and provides a more uniform upper surface. The smoothing device 144 mayeither be pivoted or rigidly mounted to the forming line frame assembly.

After smoothing, the layer of slurry has begun to set, and therespective panels 55 are separated from each other by a cutting device54, which in a typical embodiment is a water jet cutter. The cuttingdevice 54 is disposed relative to the line 10 and the frame 12 so panelsare produced having a desired length. When the speed of the carrier web14 is relatively slow, the cutting device 54 may be mounted to cutperpendicularly to the direction of travel of the web 14. With fasterproduction speeds, such cutting devices are known to be mounted to theproduction line 10 on an angle to the direction of web travel. Uponcutting, the separated panels 55 are stacked for further handling,packaging, storage and/or shipment as is well known in the art.

Another feature of the present invention is that the resultingcementitious panel (FRC panel) 55 is constructed so the fibers 34 areuniformly distributed throughout the panel. This has been found toenable the production of relatively stronger panels with relativelyless, more efficient use of fibers. The volume fraction of fibersrelative to the volume of slurry in the layer of the fiber-slurrymixture preferably constitutes approximately in the range of 1% to 5% byvolume, preferably 1.5% to 3% by volume, of the fiber-slurry mixture 46.Also, the entire final thickness of the panel is applied as a singlelayer in the form of fiber-slurry mixture to facilitate manufacturing ofthe panels 55.

Variations of the Production Line

FIG. 7 shows a composite view of a production line 110 which is a firstvariation of a process flow chart for the portion of the cementitiouspanel production line suitable for use with the present fiber-slurrymixing device upstream of the headbox and a top view of the productionline downstream of the headbox. This adds a slurry accumulator andpositive displacement pump 30.

FIG. 8 shows a composite view of a production line 210 which is a secondvariation of a process flow chart for the portion of the cementitiouspanel production line suitable for use with the present fiber-slurrymixing device upstream of the headbox and a top view of the productionline downstream of the headbox. This adds fiber roving choppers 40A.

It is contemplated that the fiber-slurry mixer 32 and fiber-slurrymixture 36 in these embodiments, and other like numbered elements shownare the same as used in the production line 10 of FIG. 5 and FIG. 6.

Although, FIGS. 5-8 show process flow diagrams for a manufacturingprocess that utilizes the fiber-slurry mixer of this invention forproducing fiber reinforced cementitious panels. Other uses andapplications of the fiber-slurry mixer of this invention are possibleand contemplated as part of this disclosure.

The fiber reinforced cementitious slurry mixtures produced using themulti-stage continuous mixer of the present invention are particularlyuseful in a variety of civil engineering and construction applications.More specifically, the fiber reinforced cementitious slurry mixturesproduced using the multi-stage continuous mixer of the present inventionare particularly useful for producing a variety of fiber reinforcedcementitious products using continuous manufacturing processes. Selectedexamples of fiber reinforced cementitious products that can be producedutilizing the material from the multi-stage continuous mixer of thepresent invention are highlighted as follows:

-   -   Structural Subfloor Panels    -   Structural Roof Sheathing Panels    -   Structural Wall Sheathing Panels    -   Structural Foundation Wall Panels    -   Permanent Formwork Panels    -   Roof Cover Board    -   Impact and Blast Resistant Panels    -   Exterior Siding Panels and Trims    -   Exterior Façade & Architectural Panels    -   Architectural Ceiling Panels    -   Roofing Tiles    -   Tile Backerboard    -   Synthetic Stone, Bricks and Tiles    -   Countertops    -   Furniture

Prefabricated Wall Assemblies, Floor and Floor-Ceiling Assemblies, andRoof Assemblies

An Alternative Product to Plywood, Oriented-Strand Board, and Low-,Medium- and High-Density Fiber Boards in Various Applications

Access Floor Panels

OTHER USES

While a particular embodiment of the present slurry feed invention forfiber-reinforced structural cementitious panel production has been shownand described, it will be appreciated by those skilled in the art thatchanges and modifications may be made thereto without departing from theinvention in its broader aspects and as set forth in the followingclaims.

What is claimed is:
 1. A continuous method for preparing cementcomposite slurry comprising the steps of: feeding a dry cementitiouspowder into a horizontal continuous fiber-slurry mixer through at leastone dry cementitious powder inlet port; the horizontal continuousfiber-slurry mixer comprising a horizontally oriented elongated mixingchamber, the elongated mixing chamber defined by a horizontal housinghaving an interior side wall, the elongated mixing chamber having anupstream end feed section, a first mixing section, and a seconddownstream end mixing section, wherein the first mixing section isbetween the upstream end feed section and the second downstream endmixing section, at least a pair of horizontally oriented intermeshingself-wiping impellers traversing from an upstream end of the elongatedmixing chamber to a downstream end of the elongated mixing chamber androtating within the elongated mixing chamber, wherein each horizontallymounted impeller within the upstream end feed section of the elongatedmixing chamber comprises an auger, wherein the dry cementitious powderis fed into the upstream end feed section of the elongated mixingchamber and conveyed by the auger to the first mixing section, feeding aliquid stream comprising water into the elongated mixing chamber of thecontinuous fiber-slurry mixer through at least one liquid stream inletport downstream of the at least one dry cementitious powder inlet portand mixing the dry cementitious powder and the liquid stream in thefirst mixing section to form a cementitious slurry; wherein eachhorizontally mounted impeller within the first mixing section comprisesa first plurality of mixing paddles mounted on a horizontally orientedshaft of the impeller at regular intervals and different circumferentiallocations, the paddles rotated about the horizontally oriented shaftwithin the horizontal housing, the paddles extending radially from theshaft, feeding a stream of reinforcement fibers through at least onereinforcement fiber inlet port into the second mixing section, andmixing the cementitious slurry and the reinforcement fibers in thesecond mixing section to form a fiber-slurry mixture, wherein at least aportion of each horizontally mounted impeller within the second mixingsection of the elongated mixing chamber comprises at least one memberselected from the group consisting of: an auger, and a second pluralityof mixing paddles mounted on the horizontally oriented shaft of thefiber-slurry mixer at regular intervals and different circumferentiallocations, the paddles rotated about each respective horizontallyoriented shaft within the horizontal housing, the paddles extendingradially from the respective shaft, discharging the fiber-slurry mixturedirectly from the second downstream end mixing section of thefiber-slurry mixer laterally relative to the horizontal housing throughan opening in the sidewall of the horizontal housing into and through afiber-slurry mixture outlet port on the horizontal housing at adownstream end portion of the second mixing section, wherein thecementitious slurry and fibers are mixed in the elongated mixing chamberof the horizontal continuous fiber-slurry mixer for an average mixingresidence time of about 5 to about 240 seconds while the rotatingpaddles apply shear force, wherein each said horizontally oriented shaftrotates at 30 to 450 RPM during mixing, to produce a uniformfiber-slurry mixture, wherein the fiber-slurry mixture discharged fromthe fiber-slurry mixer has a slump of 4 to 11 inches as measuredaccording to a slump test using a 4 inch tall and 2 inch diameter pipeand a viscosity less than 45000 centipoise when measured using aBrookfield Viscometer, Model DV-II+ Pro with Spindle HA4 attachmentrunning at 20 RPM speed.
 2. The method of claim 1, wherein the mixingchamber provides an average slurry residence time of 10 to about 60seconds.
 3. The method of claim 1, wherein the central rotating shaftrotates at 50 to 250 RPM during mixing.
 4. The method of claim 1,wherein the fiber-slurry mixtures discharged from the fiber-slurry mixerhave the viscosity of less than 10000 centipoise.
 5. The method of claim1, wherein the paddles of the first and/or second mixing sections areselected from the group consisting of flat paddles and helical paddles,wherein the flat paddles and helical paddles are unitary paddles havinga central opening fitted to the shaft such that the paddle encircles aportion of the shaft, wherein the flat paddles and helical paddles haveopposed ends extending in opposite directions from the shaft, whereinthe flat paddles or helical paddles are employed in the second mixingsection in a paddle portion of the second mixing section and an auger isalso employed in the second mixing section before and/or after thepaddle section.
 6. The method of claim 1, wherein the wherein paddles onboth shafts are used in the first mixing section, wherein augers orpaddles on both shafts are used in a first portion of the second mixingsection followed by paddles mounted on both shafts in a second portionof the second mixing section at the downstream end portion of the secondmixing section, wherein the second portion of the second mixing sectionmixes the cementitious slurry and the reinforcement fibers, wherein thesecond portion of the second mixing section extends to the downstreamend of the horizontal housing such that at least some paddles of thesecond portion of the second mixing section are above the dischargeport, wherein the second portion of the second mixing section has anabsence of an auger and no auger is downstream of the paddles of thesecond portion of the second mixing section, wherein the paddles of thesecond portion of the second mixing section are selected from the groupconsisting of helical paddles, flat paddles, paddles made of a pinhaving opposed ends, one end for attaching to the shaft and the otherend for attachment to a broad paddle head, and the pins used without thepaddle head, wherein the flat paddles and helical paddles are unitarypaddles having a central opening fitted to the shaft such that thepaddle encircles a portion of the shaft, wherein the flat paddles andhelical paddles have opposed ends extending in opposite directions fromthe shaft.
 7. The method of claim 6, wherein the paddles mounted on theindividual shafts are in over-lapping but non-interfering orientationwhen the mixer shafts are in rotational mode during the fiber-slurrymixer operation, wherein the second mixing section has an absence of anauger.
 8. The method of claim 6, wherein the first and second mixingsections have a configuration: wherein paddles on both shafts are usedin the first mixing section and wherein augers on both shafts are usedin the first portion of the second mixing section followed by helical orflat paddles mounted on both shafts in the second portion of the secondmixing section.
 9. The method of claim 6, wherein paddles are used inthe first mixing section and wherein augers on both shafts are used inthe first portion of the second mixing section followed by helicalpaddles mounted on both shafts the second portion of the second mixingsection, wherein some of the helical paddles are reversed.
 10. Themethod of claim 6, wherein flat and/or helical paddles are on the shaftin the second mixing section and all adjacent flat and/or helicalpaddles on the shaft in the second mixing section have a degree rotationwith respect to each other of 0 to 90 degree.
 11. The method of claim 6,wherein flat and/or helical paddles are on the shaft in the secondmixing section and all adjacent flat and/or helical paddles on the shaftin the second mixing section have a degree rotation with respect to eachother of 0 to 90 degree.
 12. The method of claim 6, wherein flat and/orhelical paddles are on the shaft in the second mixing section and thenumber of flat and/or helical paddles in the second mixing section isbetween 1 and
 10. 13. The method of claim 6, wherein at least some ofthe paddles in at least one member of the group consisting of the firstsection and the second section comprise pins without heads.
 14. Themethod of claim 6, wherein paddles in the first mixing section are flator helical and paddles in the second mixing section comprise paddleswith a pin and a head and/or paddles with pins.
 15. The method of claim1, wherein the paddle of the first and/or second mixing sectionscomprise a pin engaged to a paddle head, the pin pivotally engaged tothe horizontally oriented shaft and/or the paddle head to permit pivotalrotation of the paddle head relative to the respective location on thehorizontally oriented shaft, wherein the plurality of paddles arearranged to mix the reinforcement fibers and cementitious slurry andmove the cementitious slurry and reinforcement fibers being mixed to thefiber-slurry mixture outlet, wherein the paddles of the first and secondmixing section each comprise the pin engaged to the paddle head and thesecond mixing section has an absence of an auger.
 16. The method ofclaim 1, wherein the paddle of the first and/or second mixing sectionscomprise a pin engaged to a paddle head, the pin pivotally engaged tothe horizontally oriented shaft and/or the paddle head to permit pivotalrotation of the paddle head relative to the respective location on thehorizontally oriented shaft, wherein the plurality of paddles arearranged to mix the reinforcement fibers and cementitious slurry andmove the cementitious slurry and reinforcement fibers being mixed to thefiber-slurry mixture outlet, wherein the paddles of the first and secondmixing section each comprise the pin engaged to the paddle head and thesecond mixing section has an absence of an auger, wherein orientation ofthe paddle head having a broad surface with respect to the central shaftvertical cross-section is from about 10° to 80°.
 17. The method of claim1, wherein the overall dimensions of the paddles are such that theclearance (space) between the inner circumference of the fiber-slurrymixer chamber and the paddle's furthermost point from the central shaftis less than ¼″.
 18. The method of claim 1, wherein the cementitiousslurry and fibers are mixed in the mixing chamber of the fiber-slurrymixer to produce the uniform fiber-slurry mixture that has consistencythat will allow the fiber-slurry mixture to be discharged from thefiber-slurry mixer and be suitable for being deposited from a headbox asa continuous curtain on a moving surface of a panel production lineuniformly as a layer 0.4 to 1.25 inches thick on the moving surface ofthe panel production line to produce a fiber reinforced concrete panel,further comprising passing the discharged slurry into the headbox,depositing the slurry from the headbox onto the continuous movingsurface, and vibrating the deposited slurry with a vibrating plate toassist in leveling the fiber-slurry mixture, the vibrating plate isprovided under or slightly downstream of the location where the headboxdeposits the fiber-slurry mixture.
 19. The method of claim 1, whereinthe paddles and shell the horizontal housing interior side wall arecoated with a release material, to minimize buildup of the cementitiousslurry on the paddles.
 20. The method of claim 1, wherein the mixingchamber of the fiber-slurry mixer adapted and configure to mix thecementitious slurry and fibers in the mixing chamber of the fiber-slurrymixer for an average mixing residence time of about 10 to about 120seconds, while the rotating paddles apply shear force to thefiber-slurry and length of the mixing chamber ranges from 3 to 8 feet,and diameter of the mixing chamber ranges from about 6 to 24 inches.